Low-permeation flexible fuel hose

ABSTRACT

A flexible hose or a tubing having a barrier layer of polyamide 6 having an impact modifier, and/or branched molecular structure, a flexural modulus of 1 to 2 GPa and/or a tensile elongation of 100% or more. The hose may have additional layers such as an HNBR rubber inner tube, an EVM/CPE rubber blend outer cover, a textile or wire reinforcement, or the like. Permeability to ethanol- and methanol-containing fuels is very low. Permeability to B20 biofuels is very low.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. application Ser. No.13/116,879, which claims the benefit of U.S. Provisional ApplicationSer. No. 61/352,822 filed Jun. 8, 2010, and which also is acontinuation-in-part of U.S. application Ser. No. 12/791,654 filed onJun. 1, 2010, which claims the benefit of U.S. Provisional ApplicationSer. No. 61/296,784 filed on Jan. 20, 2010, and the benefit of U.S.Provisional Application Ser. No. 61/183,030 filed on Jun. 1, 2009.

BACKGROUND OF THE INVENTION

Field of the Invention

This invention relates generally to a flexible fuel hose with lowpermeability to fuels, and more particularly to a hose with a barrierlayer of a particular type of polyamide 6.

Description of the Prior Art

The increased used of motor-vehicle fuels containing alcohol, includingethanol, along with stringent emissions standards for fuel systemcomponents has necessitated improvement over conventional flexible hoseconstructions. Conventional fuel hose constructions used economical,fuel-resistant rubber materials such as nitrile rubber (NBR),nitrile-polyvinyl chloride blends (NBR-PVC), epichlorohydrin (ECO), andthe like. Improved hose for alcohol-containing fuels now generally useone or more of various fluoroelastomers and/or fluoroplastics such asthose commonly designated as FKM, PVDF, ETFE, FEP, EFEP, PCTFE, THV,PTFE, and the like (hereinafter referred to generally as fluoropolymers)to provide a barrier to alcohol and fuel permeation. The typicalpreferred material for a fuel hose barrier layer is a fluoropolymer filmsuch as THV (a terpolymer of tetrafluoroethylene, hexafluoropropylene,and vinylidene fluoride) an example of which is disclosed in U.S. Pat.No. 5,679,425.

While fluoropolymer barrier hose has dominated the fuel hose market,many other materials are available as potential barrier layers. U.S.Pat. No. 6,945,279, which is directed to a method of making rubber hoseswith an intermediate thermoplastic layer by rolling a planar resin filminto a cylindrical layer with an overlap, discloses extensive lists ofpotential rubber materials and thermoplastic resin materials. While NBRis mentioned on the list of potential rubber materials and polyamide 6(“PA 6”) as a potential resin film, U.S. Pat. No. 6,945,279 offers noparticular guidance for selecting materials for any particular use, andno working examples are disclosed therein. Typical fuel hoses havefurther included multi-layer barrier constructions which combinefluoropolymers with other materials including for example polyamides.Frequently polyamides are cited as useful materials for thermoplasticmultilayer tubing for fuels.

An example of use of a thermoplastic film layer of nylon 11 (i.e.,polyamide 11) in fuel hose is provided by U.S. Pat. No. 6,279,615,wherein the polyamide (“PA”) is the innermost veneer layer on the innersurface of the rubber hose of a comparative example. Regardless, thepermeation rates obtained for the hose described in U.S. Pat. No.6,279,615 were not low enough to meet current SAE (Society of AutomotiveEngineers) standards. U.S. Pat. No. 2,564,602 discloses a rubber hosewith an intermediate layer of flexible, resinous, thermoplastic materialincluding nylon. U.S. Pat. Pub. No. 2007/194481A1 discloses a rubberhose with inner tube and outer cover of rubber and an intermediatebarrier resin layer of any kind of thermoplastic resin including PA 6,but preferably of fluoropolymer for fuel hose applications, wherein theresin layer is plasma treated. U.S. Pat. No. 7,478,653 discloses a4-layer rubber fuel hose with a barrier layer of fluoropolymer orpolyamide (including PA 6).

U.S. Pat. No. 6,855,787 discloses thermoplastic fuel transfer tubesbased on polyamide resin, such as PA 6, containing a barrier layer offluoropolymer. U.S. Pat. No. 6,491,994 discloses a thermoplastic fueltransfer tube based on layers of PA 11 or PA 12 resin, PA 6, and PA 6with a layered silicate dispersed therein. U.S. Pat. No. 7,011,114discloses a thermoplastic fuel transfer tube based on polyamide resincontaining a barrier layer of polyphenylene sulfide (“PPS”).

An example of use of a multi-layer barrier is disclosed in U.S. Pat. No.5,038,833, wherein the primary application is rigid plastic pipes. Anexample of use in a refrigerant hose of a thermoplastic barrier layer isprovided by U.S. Pat. No. 6,941,975, wherein the barrier layer requirestwo or three layers, including a layer of vinyl resin such asethylene-vinyl alcohol copolymer (“EVOH”) and outer layers of polyolefinand/or polyamide resin. Each resin layer has a thickness of from 0.025to 0.25 mm. The only example provided in U.S. Pat. No. 6,941,975 used a3-layer barrier with 0.15-mm total thickness and had a permeation ratefor R134 refrigerant of 3.94×10⁻⁵ g/cm/day based on a one-cm length ofhose of undisclosed diameter. U.S. Pat. No. 7,504,151 discloses arefrigerant hose with a barrier layer of PA 6/66 copolymer, PA 11, PA12, PA 6, or PA 6/12 compounded with nanofillers. U.S. Pat. No.7,478,654 discloses a refrigerant barrier hose with a 2-layer barrierthat includes as one of the layers a thermoplastic resin such as PA 6 orone of many others.

Reference is made to co-pending U.S. patent application Ser. No.11/938,139 filed on Nov. 9, 2007, the entire contents of which arehereby incorporated herein by reference. That application discloses aflexible fuel hose having a non-fluorinated rubber inner tube, anon-fluorinated rubber outer cover, an intermediate barrier layerconsisting essentially of EVOH having an ethylene content less than 30mole %, and preferably a textile reinforcement between the barrier layerand the outer cover. A non-fluorinated rubber tie layer may be includedbetween the barrier and the reinforcement. Permeability to ethanol- andmethanol-containing fuels is very low. The EVOH layer may be extrudedonto an unvulcanized rubber inner tube and an unvulcanized rubber outercover extruded thereon. However, during handling of the resulting rawhose before and during vulcanization, the stiffness of the EVOH layercan result in kinking, delamination and other processing problems. As aresult of this stiffness, EVOH-based hose failed the SAE J30R14 kinktest.

SUMMARY

The present invention is directed to systems and methods which provide alow-permeation fuel hose suitable for example for use withalcohol-containing fuels and which is very flexible and easier tomanufacture without kinking or delamination. The invention furtherprovides an economical fuel hose in that fluorinated materials are notrequired. Specifically the present invention provides a very lowpermeation rubber fuel hose based on non-fluorinated elastomer with anintermediate PA 6 barrier layer, optionally reinforced with eithertextile or wire. The present invention may be embodied in a lowpermeation fuel hose with a barrier layer of PA 6 having a non-linear orbranched molecular structure and an impact modifier with no additionalthermoplastic or fluorinated-polymer barrier layers. Alternately, the PA6 barrier layer may have a flexural modulus of about 2 GPa or less andan elongation of about 100% or more. The PA 6 barrier layer may beTechnyl® C 548B, which is sold under that trademark by RhodiaEngineering Plastics.

Embodiments of the present invention are directed to a fuel hosecomprising a rubber inner tube, an intermediate barrier layer comprisingPA 6 having a branched molecular structure and an impact modifier, and arubber outer cover. The barrier layer may consist essentially of the PA6 layer or may consist of the PA 6 layer. The thickness of the barrierlayer may be in the range from 0.025-0.76 mm (1 to 30 mils), preferablyfrom 0.025-0.38 mm (1 to 15 mils), or from 0.07-0.18 mm (3 to 7 mils),or up to 10 mils thick. The inner tube and outer cover may compriseacrylonitrile-butadiene rubber (NBR), hydrogenatedacrylonitrile-butadiene rubber (HNBR), epichlorohydrin rubber (ECO),chlorosulfonated polyethylene (CSM), polychloroprene rubber (CR),chlorinated polyethylene (CPE), ethylene-vinyl acetate (EVM), ornitrile-polyvinylchloride (NBR-PVC) blended elastomer, thermoplasticelastomer (TPE), and the like. Both of the inner tube and a tie layermay comprise the same rubber composition. Preferably, neither the innertube, the tie layer, the outer cover, nor the barrier layer needcomprise fluoropolymer. Textile or wire reinforcement may be applieddirectly to the PA 6 barrier layer, or to a friction or tie layer whichmay be applied to the barrier layer prior to the reinforcement. Anadhesion system, such as a resorcinol, formaldehyde donor, and silica(RFS) system, may be used in the friction layer and/or the inner tubelayer to promote adhesion to the PA 6. The need for reinforcement may besignificantly reduced by the PA 6 barrier layer due to an increase inburst strength.

In another embodiment, the inventive hose may comprise two or morelayers, or two to five layers, including a thin layer of PA 6 asdescribed herein. The PA 6 layer may preferably have a thickness of upto 0.010 inches (0.25 mm). The PA 6 may preferably be of sufficientthickness, or an effective thickness, to provide reduced permeation of aspecified or predetermined fuel or fuel component of less than or equalto 15 grams per square meter per day. The predetermined fuel componentmay be methanol or ethanol. The other layers may be or include areinforcement such as a textile or wire, a different thermoplasticmaterial including for example a TPE, a thermoset material such as arubber or a crosslinked thermoplastic.

The present invention is also directed to a hose assembly or fuel systememploying a fuel hose according to the above description and at leastone fitting, such as a clamp, coupling, connector, nipple, tubing, orthe like, and/or a fuel or fluid handling component such as a tank,pump, canister, rail, or injector or the like.

The foregoing has outlined rather broadly the features and technicaladvantages of the present invention in order that the detaileddescription of the invention that follows may be better understood.Additional features and advantages of the invention will be describedhereinafter which form the subject of the claims of the invention. Itshould be appreciated by those skilled in the art that the conceptionand specific embodiment disclosed may be readily utilized as a basis formodifying or designing other structures for carrying out the samepurposes of the present invention. It should also be realized by thoseskilled in the art that such equivalent constructions do not depart fromthe spirit and scope of the invention as set forth in the appendedclaims. The novel features which are believed to be characteristic ofthe invention, both as to its organization and method of operation,together with further objects and advantages will be better understoodfrom the following description when considered in connection with theaccompanying figures. It is to be expressly understood, however, thateach of the figures is provided for the purpose of illustration anddescription only and is not intended as a definition of the limits ofthe present invention.

BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying drawings, which are incorporated in and form part ofthe specification in which like numerals designate like parts,illustrate embodiments of the present invention and together with thedescription, serve to explain the principles of the invention. In thedrawings:

FIG. 1 is a partially fragmented perspective view of an embodiment of ahose constructed in accordance with the present invention;

FIG. 2 is a schematic of an embodiment of a hose system constructed inaccordance with the present invention; and

FIG. 3 is a partially fragmented perspective view of another embodimentof a hose constructed in accordance with the present invention.

DETAILED DESCRIPTION

Referring to FIG. 1, a hose is illustrated, constructed according to oneembodiment of the present invention. Hose 11 comprises inner tube 12,intermediate thermoplastic barrier layer 14 of polyamide 6 (PA 6), andouter cover 16. Optionally, hose 11 may comprise reinforcement layer 18positioned somewhere within the hose. As another option, hose 11 maycomprise one or more tie layers and/or adhesive coatings between variouslayers. FIG. 1 shows reinforcement layer 18 applied over tie layer 20.Intermediate layer 14 could be disposed within one of the rubber layers,thus effectively splitting that rubber layer into two separate layers.

Intermediate barrier layer 14 comprises PA 6 preferably having abranched molecular structure, i.e., not a linear polymeric structure.The thickness of the intermediate layer may be in the range from 0.025to 0.76 mm (1 to 30 mils), preferably from 0.025 to 0.38 mm (1 to 15mils), or from 0.05 to 0.25 mm (2 to 10 mils). PA 6 is believed to be agood permeation barrier to gases because it is a semi- to highlycrystalline polymer and because of the high cohesive energy of the amidegroups. Generally, the higher the crystallinity, the lower thepermeability. However, high crystallinity makes PA 6 a brittle, rigidpolymer with poor low-temperature flexibility. The higher the branchingin the PA 6, the lower the crystallinity and the higher the flexibility.The presence of impact modifier also increases flexibility. Thus, priorapplications have used rigid PA 6 grades as a rigid structural materialand/or have used thin conventional PA 6 layers coupled with additionallayers of other barrier materials such as fluoropolymers, polyolefins,EVOH, and/or the like. However, in accordance with embodiments of thepresent invention, a flexible fuel hose with exceptionally lowpermeability to various fuels such as indolene, gasoline, biodiesel,diesel, alcohols, and alcohol-containing fuels, can be constructed usinga single barrier layer comprising or even consisting essentially of orconsisting of PA 6, preferably PA 6 having a branched structure and animpact modifier or having a flexural modulus of about 2 GPa or less andan elongation of about 100% or more.

PA 6 is also variously identified as polycaprolactam, nylon 6, andpolycaproamide. Herein, the term PA 6, or “comprising PA 6” could alsoinclude polymer blends of PA 6 and other polymers. For example, withoutlimitation, PA 6 herein could include blends of PA 6 with one or more ofPA 11, PA 12, PA 66, PA 610, PA 612, PA 46, and the like. In addition,the blends could include impact modifiers or other additives such asthose described herein. Alternately, PA 6 herein could be substantiallyPA 6 without any other blended polymers other than impact modifiers.

Regarding the aforementioned cohesive energy of the amide groups, PA 6may exhibit an associated sensitivity to moisture, resulting inincreased permeability in high humidity environments. Such humidenvironments may be present at almost any time during the life of ahose, from a steam vulcanization environment during manufacture of ahose to the place of use in a vehicle in a wet or humid climate. Inaccordance with embodiments of the present invention, the use ofsuitable non-fluorinated rubber inner tube and outer cover layerssufficiently protects the PA 6 barrier layer from moisture. Suitablerubber compositions may be based on NBR, HNBR, CSM, CR, ECO, EVM, CPE,NBR-PVC, ethylene methylacrylate elastomer (EAM), acrylic or acrylateelastomer (ACM), or TPE, or the like. Preferred rubber compositions forthe inner tube for alcohol-containing fuels are based on NBR, NBR-PVC,ECO, and/or HNBR. It should be understood that steps may nevertheless betaken to prevent detrimental exposure to steam or moisture, such assealing the ends of the hose during vulcanization, and the like.

Suitable grades of PA 6 for the barrier layer include those with abranched molecular structure and an impact modifier. The branchedmolecular structure is believed to improve resistance to permeation bycreating or forcing a more tortuous molecular route for diffusingsubstances. The presence of impact modifier is believed to provideneeded flexibility for processing the PA 6 and eliminating kinkingproblems and may also enhance the resistance to permeation. Preferably,suitable PA 6 for the practice of this invention has a relatively highviscosity and a relatively low melt flow rate. Suitable PA 6 maypreferably be a blow-molding grade or may be an extrusion grade.Suitable PA 6 has a melting temperature of 200-240° C. or of about 220°C. or about 222° C., which is well above the temperature at which innertube and outer cover rubber compositions are typically extruded,vulcanized or cured. Suitable PA 6 should have a relatively low flexuralmodulus, for example, flexural modulus may be in the range of less thanabout 2 GPa, or from about 1 to about 2 GPa and may be tested accordingto the test method of ISO 178. Suitable PA 6 should also have arelatively high tensile strain at break or “elongation.” For example,elongation may be in the range of about 100% or more and may be testedaccording to the test method of ISO 527.

A preferred grade of PA 6 is Technyl® C 548B, which is sold under thattrademark by Rhodia Engineering Plastics. Other suitable grades mayinclude Technyl® C 536XT and C 442, from Rhodia. As non-limitingexamples, other suitable grades may include: Capron® 8259, sold underthat trademark by BASF; and Aegis™PL220HS, sold under that trademark byHoneywell; and Renol 6253, sold under that trade name by Clariant. Table1 lists some properties of one or more suitable grades of PA 6.

TABLE 1 Values* for Technyl ® Properties Standards Units Technyl ® C548B C 536XT Physical Water absorption (24 h at 23° C.) ISO 62 % 1.20Density ISO 1183-A g/cm³ 1.05 Molding shrinkage Parallel RHODIA-EP %1.20 Molding shrinkage normal or RHODIA-EP % 1.25 perpendicular MoldingShrinkage Isotropy RHODIA-EP 0.96 Mechanical Tensile modulus ISO 527type 1 A MPa 1850/1000 2340/700  Tensile strength at yield ISO 527 type1 A MPa 55/45 60/—  Tensile strain at break ISO 527 type 1 A % 150/22055/170 Flexural modulus ISO 178 MPa 1750/850  Flexural maximum stressISO 178 MPa 70/45 Charpy notched impact strength ISO 179/1eA kJ/m² 92/NB 73/130 Charpy unnotched impact strength ISO 179/1eU kJ/m² NB/NBIzod notched impact strength ISO 180/1A kJ/m²  90/NB Thermal MeltingTemperature ISO 11357 ° C. 222    220 Heat deflection temperature, 1.8Mpa ISO 75/Af ° C. 55    56 Coef. of Linear thermal expansion normal ISO11359 10⁻⁵/° C. 7   or perpendicular (23° C. to 85° C.) Typicalprocessing Temperature RHODIA-EP ° C. 210-240 Electrical Relativepermittivity IEC 60250 3.70/4   Dissipation factor IEC 60250 0.02/0.12Volume resistivity IEC 60093 E14. Ohm · cm   10/0.001 Surfaceresistivity IEC 60093 E14. Ohm   1/0.001 Dielectric strength IEC 60243kV/mm —/17 *Where two values are indicated, the first value is for“d.a.m.” i.e., Dry As Molded compound, and the second value is formaterial conditioned according ISO 1110.

Useful grades of PA 6 may have one or more impact modifiers. Impactmodifiers for polyamide include natural and synthetic polymer substancesthat are elastomeric or rubbery at room temperature and may also have atensile modulus of elasticity of less than 500 MPa as measured inaccordance with ASTM D882. The impact modifier may, for example, be an(ethylene and/or propylene)/α-olefin copolymer; an (ethylene and/orpropylene)/(α,β-unsaturated carboxylic acid and/or an unsaturatedcarboxylic acid ester) copolymer; an ionomer polymer; an aromatic vinylcompound/a conjugated diene compound block copolymer or a polyamideelastomer. These materials may be used alone or in blends.

The above-mentioned (ethylene and/or propylene)/α-olefin copolymer is apolymer obtained by copolymerizing ethylene and/or propylene with anα-olefin having at least 3 carbon atom. The α-olefin having at least 3carbon atom may be propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene,1-octene, 1-nonene, 1-decene, 1-undecene, 1-dodecene, 1-tridecene,1-tetradecene, 1-pentadecene, 1-hexadecene, 1-heptadecene, 1-octadecene,1-nonadecene, 1-eicosene, 3-methyl-1-butene, 4-methyl-1-butene,3-methyl-1-pentene, 3-ethyl-1-pentene, 1-methyl-1-pentene,4-methyl-1-hexene, 4,4-dimethyl-1-hexene, 4,4-dimethyl-1-pentene,4-ethyl-1-hexene, 3-ethyl-1-hexene, 9-methyl-1-decene,11-methyl-l-dodecene or 12-ethyl-1-tetradecene, or a combinationthereof.

Further, a polyene of a non-conjugated diene such as 1,4-pentadiene,1,4-hexadiene, 1,5-hexadiene, 1,4-octadiene, 1,5-octadiene,1,6-octadiene, 1,7-octadiene, 2-methyl-1,5-hexadiene,6-methyl-1,5-heptadiene, 7-methyl-1,6-octadiene,4-ethylidene-8-methyl-1,7-nonadiene, 4,8-dimethyl-1,4,8-decatriene(DMDT), dicyclopentadiene, cyclohexadiene, dicyclobutadiene, methylenenorbornene, 5-vinyl norbornene, 5-ethylidene-2-norbornene,5-methylene-2-norbornene, 5-isopropylidene-2-norbornene,6-chloromethyl-5-isopropenyl-2-norbornene,2,3-diisopropylidene-5-norbornene,2-ethylidene-3-isopropylidene-5-norbornene or2-propenyl-2,2-norbornadiene, may be copolymerized as a third monomerfor example to provide crosslinking sites.

The above-mentioned (ethylene and/or propylene)/(an α,β-unsaturatedcarboxylic acid and/or an unsaturated carboxylic acid ester) copolymeris a polymer obtained by copolymerizing ethylene and/or propylene withan α,β-unsaturated carboxylic acid and/or an unsaturated carboxylic acidester monomer. The α,β-unsaturated carboxylic acid monomer may beacrylic acid or methacrylic acid, and the α,β-unsaturated carboxylicacid ester monomer may be a methyl ester, an ethyl ester, a propylester, a butyl ester, a pentyl ester, a hexyl ester, a heptyl ester, anoctyl ester, a nonyl ester or a decyl ester of such an unsaturatedcarboxylic acid, or a mixture thereof.

The above-mentioned ionomer polymer is one having at least some ofcarboxyl groups of a copolymer of an olefin with an α,β-unsaturatedcarboxylic acid ionized by neutralization with metal ions. As theolefin, ethylene is preferably employed, and as the α,β-unsaturatedcarboxylic acid, acrylic acid or methacrylic acid is preferablyemployed. However, they are not limited to those exemplified here, andan unsaturated carboxylic acid ester monomer may be copolymerizedthereto. Further, the metal ions may, for example, be Al, Sn, Sb, Ti,Mn, Fe, Ni, Cu, Zn or Cd, in addition to an alkali metal or an alkalineearth metal, such as Li, Na, K, Mg, Ca, Sr or Ba.

Further, the aromatic vinyl compound/a conjugated diene compoundblock-copolymer is a block copolymer comprising aromatic vinyl compoundpolymer blocks and conjugated diene compound polymer blocks, and a blockcopolymer having at least one aromatic vinyl compound polymer block andat least one conjugated diene compound polymer block, is employed.Further, in such a block copolymer, the unsaturated bond in theconjugated diene compound polymer block may be hydrogenated.

The aromatic vinyl compound polymer block is a polymer block composedmainly of structural units derived from an aromatic vinyl compound. Insuch a case, the aromatic vinyl compound may, for example, be styrene,α-methylstyrene, o-methylstyrene, m-methyl styrene, p-methyl styrene,1,3-dimethyl styrene, 2,4-dimethylstyrene, vinyl naphthalene, vinylanthracene, 4-propylstyrene, 4-cyclohexyl styrene, 4-dodecylstyrene,2-ethyl-4-benzyl styrene or 4-(phenylbutyl)styrene. The aromatic vinylcompound polymer block may have structural units made of one of moretypes of the above-mentioned monomers. Further, the aromatic vinylcompound polymer block may have structural units made of a small amountof other unsaturated monomers, as the case requires.

The conjugated diene compound polymer block is a polymer block formed ofone or more types of conjugated diene compounds such as 1,3-butadiene,chloroprene, isoprene, 2,3-dimethyl-1,3-butadiene, 1,3-pentadiene,4-methyl-1,3-pentadiene and 1,6-hexadiene. In the hydrogenated aromaticvinyl compound/conjugated diene block copolymer, some or all ofunsaturated bond portions in the conjugated diene compound polymer blockare hydrogenated to saturated bonds. Here, the distribution in thepolymer block composed mainly of a conjugated diene may be random,tapered, partially blocked or an optional combination thereof.

The molecular structure of the aromatic vinyl compound/conjugated dienecompound block copolymer or its hydrogenated product, may be linear,branched, radial or an optional combination thereof. Among them, in thepresent invention, as the aromatic vinyl compound/conjugated diene blockcopolymer and/or its hydrogenated product, at least one of a diblockcopolymer wherein one aromatic vinyl compound polymer block and oneconjugated diene compound polymer block are linearly bonded; a triblockcopolymer wherein three polymer blocks are linearly bonded in the orderof an aromatic vinyl compound polymer block/conjugated diene compoundpolymer block/aromatic vinyl compound polymer block; and theirhydrogenated products, is preferably employed. Specifically, anon-hydrogenated or hydrogenated styrene/butadiene copolymer, anon-hydrogenated or hydrogenated styrene/isoprene copolymer, anon-hydrogenated or hydrogenated styrene/isoprene/styrene copolymer, anon-hydrogenated or hydrogenated styrene/butadiene/styrene copolymer ora non-hydrogenated or hydrogenated styrene/(isoprene/butadiene)/styrenecopolymer may, for example, be mentioned.

The above-mentioned polyamide elastomer is a block copolymer comprisingmainly polyamide-forming units as hard segments and polyether units orpolyether ester units formed by polycondensation of a polyether with adicarboxylic acid, as soft segments. It may, for example, be a polyetherester amide elastomer or a polyether amide elastomer. Thepolyamide-forming unit as such a hard segment may, for example, be alactam of at least 3-membered ring, an aminocarboxylic acid or a nylonsalt made of a dicarboxylic acid and a diamine. The lactam of at least3-membered ring may, for example, be ε-caprolactam or laurolactam. Theaminocarboxylic acid may, for example, be 6-aminocaproic acid,11-aminoundecanoic acid or 12-aminododecanoic acid.

As the dicarboxylic acid to constitute the nylon salt, a C₂₋₃₆dicarboxylic acid is usually employed. Specifically, it may, forexample, be an aliphatic dicarboxylic acid such as adipic acid, pimelicacid, suberic acid, azelaic acid, sebacic acid, undecanedione acid,dodecanedione acid or 2,2,4-trimethyladipic acid; an alicyclicdicarboxylic acid such as 1,4-cyclohexanedicarboxylic acid; or anaromatic dicarboxylic acid such as terephthalic acid, isophthalic acid,phthalic acid or xylene dicarboxylic acid. Further, as a C.sub.36dicarboxylic acid, a dimeric fatty acid may be mentioned. The dimericfatty acid is a polymerized fatty acid obtainable by polymerizing e.g. aC₈₋₂₄ saturated, ethylenically unsaturated, acetylenically unsaturated,natural or synthetic monobasic fatty acid.

As the diamine to constitute the nylon salt, a C₂₋₃₆ diamine is usuallyemployed. Specifically, it may, for example, be an aliphatic diaminesuch as ethylenediamine, trimethylenediamine, tetramethylenediamine,pentamethylenediamine, hexamethylenediamine, heptamethylenediamine,octamethylenediamine, nonamethylenediamine, decamethylenediamine,undecamethylenediamine, dodecamethylenediamine or2,2,4/2,4,4-trimethylhexamethylenediamine; an alicyclic diamine such as1,3/1,4-cyclohexanedimethylamine or bis(4,4′-aminocyclohexyl)methane; oran aromatic diamine such as xylylene diamine. Further, as a C₃₆ diamine,a dimeric amine having carboxyl groups of the dimeric fatty acid changedto amino acids, may be mentioned.

Further, the polyether unit as a soft segment may, for example, bepolyethylene glycol, polypropylene glycol, polytetramethylene glycol,polyhexamethylene glycol tetrahydrofuran or a copolymer prepared byusing a plurality of such polyether-forming monomers.

The polyether ester amide elastomer is a polyamide elastomer comprisingthe above polyether and the above polyamide-forming unit having terminalcarboxyl groups prepared by introducing the above-mentioned dicarboxylicacid. Further, the polyether amide elastomer is a polyamide elastomercomprising a polyether unit obtained by substituting an amino groupand/or a carboxyl group for the terminal hydroxyl group of theabove-mentioned polyether, and a polyamide-forming unit having acarboxyl group and/or an amino terminal group.

Further, the above-mentioned (ethylene and/or propylene)/α-olefincopolymer, the (ethylene and/or propylene)/(α,β-unsaturated carboxylicacid and/or unsaturated carboxylic ester) copolymer, the ionomerpolymer, the block copolymer of an aromatic vinyl compound and aconjugated diene compound, to be used as an impact modifier, is employedpreferably in the form of a polymer modified by a carboxylic acid and/orits derivative.

As the carboxylic acid and/or its derivative to be used for themodification, a carboxylic acid group, a carboxylic anhydride group, acarboxylic acid ester group, a carboxylic acid metal salt group, acarboxylic acid imide group, a carboxylic acid amide group or an epoxygroup may, for example, be mentioned. Examples for a compound containingsuch a functional group include acrylic acid, methacrylic acid, maleicacid, fumaric acid, itaconic acid, crotonic acid, methyl maleic acid,methyl fumaric acid, metaconic acid, citraconic acid, glutaconic acid,cis-4-cyclohexene-1,2-dicarboxylic acid,endcis-bicyclo[2,2,1]hepto-5-ene-2,3-dicarboxylic acid and metal saltsof these carboxylic acids, monomethyl maleate, monomethyl itaconate,methyl acrylate, ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate,hydroxyethyl acrylate, methyl methacrylate, 2-ethylhexyl-methacrylate,hydroxyethyl methacrylate, aminoethyl methacrylate, dimethyl maleate,dimethyl itaconate, maleic anhydride, itaconic anhydride, citraconicanhydride, endobicyclo-[2,2,1]-5-heptene-2,3-dicarboxylic acidanhydride, maleimide, N-ethyl maleimide, N-butyl maleimide, N-phenylmaleimide, acrylamide, methacrylamide, glycidyl acrylate, glycidylmethacrylate, glycidyl ethacrylate, glycidyl itaconate and glycidylcitraconate.

By the use of impact modified PA 6, the resulting hose should have goodflexibility and kink resistance. The amount of the impact modifier maybe from 1 to 25% by weight, preferably from 3 to 10%, based on the totalweight of the polyamide compound. If the amount of the impact modifierexceeds 25%, the strength of the material may tend to decrease.

Thus the impact modifier for the polyamide may be an elastomer or arubbery polymer, preferably grafted with functional groups chosen fromcarboxylic acids and acid anhydrides. The grafting of acid anhydridefunctions of copolymers is generally achieved by copolymerization in thepresence of maleic anhydride.

The rubbery polymers which may be used as impact modifiers may bealternately or additionally defined as having a tensile modulus to ASTMD-638 of less than about 40,000 MPa, generally less than 25,000, andpreferably less than 20,000. They may be random or block copolymers.Useful rubbery polymers may be prepared from reactive monomers which canbe part of the chains or branches of the polymer, or can be grafted ontothe polymer. These reactive monomers may be dienes or carboxylic acidsor their derivatives, such as esters or anhydrides. Amongst theserubbery polymers mention may be made of butadiene polymers, copolymersof butadiene/styrene, isoprene, chloroprene, copolymers ofacrylonitrile/butadiene, isobutylene, copolymers ofisobutylene-butadiene or copolymers of ethylene/propylene (EPR),copolymers of ethylene/propylene/diene (EPDM). As useful rubberypolymers mention may be made of aromatic vinylic monomers, olefins,acrylic acid, methacrylic acid and derivatives of these,ethylene-propylene-diene monomers, and metal salts of these. Some usefulrubbery polymers are described in the patents U.S. Pat. Nos. 4,315,086and 4,174,358, the relevant portions of which are hereby incorporatedherein by reference.

A preferred impact modifier for carrying out the invention is a graftedcopolymer which is a copolymer of ethylene and of an α-olefin other thanethylene having, grafted onto the ethylene copolymer, a functionalitysuch as carboxylic or anhydride functions. The ethylene and the α-olefinare preferably a copolymer of ethylene and of an α-olefin selected froman α-olefin containing from 3 to 8 carbon atoms and preferably from 3 to6 carbon atoms. A preferred α-olefin monomer in the copolymer ispropylene. Other α-olefins, such as 1-butene, 1-pentene and 1-hexene,may be used in the copolymers in place of or in addition to propylene.In one preferred manner of working the invention, mention may be made ofmaleic-anhydride-grafted ethylene-propylene rubbers andmaleic-anhydride-grafted ethylene-propylene-diene rubbers.

Alternately, the impact modifier may be selected from the groupconsisting of maleic-anhydride-grafted ethylene-propylene rubber,maleic-anhydride-grafted ethylene-propylene-diene rubber,maleic-anhydride-grafted polyethylenes, and maleic-anhydride-graftedpolypropylene.

To reduce the permeability of the polyamide 6 barrier layer, it ispossible to add lamellar nanofillers to the thermoplastic matrix. Such areduction in permeability is attributed to an effect of “tortuousness”brought about by the lamellar nanofillers. This is because the gases orthe liquids have to follow a much longer pathway because of theseobstacles arranged in successive strata. Theoretical models regard thebarrier effects as becoming more pronounced as the aspect ratio, that isto say the length/thickness ratio, increases. The lamellar nanofillerswhich are most widely investigated today are clays of smectite type,mainly montmorillonite. The difficulty of use lies first of all in themore or less extensive separation of these individual lamellae, that isto say the exfoliation, and in their distribution, in the polymer. Tohelp in the exfoliation, use may be made of an “intercalation”technique, which consists in swelling the crystals with organic cations,generally quaternary ammonium cations, which will compensate for thenegative charge of the lamellae. These crystalline aluminosilicates,when they are exfoliated in a thermoplastic matrix, exist in the form ofindividual lamellae, the aspect ratio of which may reach values of theorder of 500 or more.

The polyamide 6 of the present invention may also utilize particlesbased on zirconium, titanium, cerium and/or silicon phosphate, in theform of non-exfoliated nanometric lamellar compounds, as disclosed forexample in U.S. Pat. Pub. No. 2007/00182159A1, the relevant portions ofwhich are hereby incorporated herein by reference. Such in PA 6 exhibitsgood barrier properties to liquids and to gases and/or good mechanicalproperties, such as, for example, a good modulus/impact compromise,and/or a temperature stability which allows it to be handled and used athigh temperatures. The particles based on zirconium, titanium, ceriumand/or silicon phosphate, present in the PA 6 composition, may be suchthat at least 50% by number of the particles are in the form ofnanometric lamellar compounds exhibiting an aspect ratio of less than orequal to 100.

The term “nanometric lamellar compound” is understood to mean a stack ofseveral lamellae exhibiting a thickness of the order of severalnanometers. The nanometric lamellar compound according to the inventioncan be non-intercalated or else intercalated by an intercalation agent,also referred to as swelling agent. The term “aspect ratio” isunderstood to mean the ratio of the greatest dimension, generally thelength, to the thickness of the nanometric lamellar compound.Preferably, the particles of nanometric lamellar compounds exhibit anaspect ratio of less than or equal to 50, more preferably of less thanor equal to 10, particularly of less than or equal to 5. Preferably, theparticles of nanometric lamellar compounds exhibit an aspect ratio ofgreater than or equal to 1.

The term “a nanometric compound” is understood to mean a compound havinga dimension of less than 1 μm. Generally, the particles of nanometriclamellar compounds of use exhibit a length of between 50 and 900 nm,preferably between 100 and 600 nm, a width of between 100 and 500 nm anda thickness of between 50 and 200 nm (the length representing thelongest dimension). The various dimensions of the nanometric lamellarcompound can be measured by transmission electron microscopy (TEM) orscanning electron microscopy (SEM). Generally, the distance between thelamellae of the nanometric lamellar compound is between 0.5 and 1.5 nm,preferably between 0.7 and 1.0 nm. This distance between the lamellaecan be measured by crystallographic analytical techniques, such as, forexample, X-ray diffraction.

Advantageously, 50% by number of the particles are in the form ofnanometric lamellar compounds exhibiting an aspect ratio of less than orequal to 100. The other particles can be in particular in the form ofindividual lamellae, for example obtained by exfoliation of a nanometriclamellar compound. Preferably, at least 80% by number of the particlesare in the form of nanometric lamellar compounds exhibiting an aspectratio of less than or equal to 100. More preferably, approximately 100%by number of the particles are in the form of nanometric lamellarcompounds exhibiting an aspect ratio of less than or equal to 100.

The particles can optionally be gathered together in the form ofaggregates and/or agglomerates in the PA 6 thermoplastic matrix. Theseaggregates and/or agglomerates can in particular exhibit a dimension ofgreater than one micron.

Use may also be made, for the PA 6 of the present invention, ofparticles of hydrated nanometric lamellar compounds based on zirconium,titanium, cerium and/or silicon phosphate, such as, for example,monohydrated or dihydrated compounds. Use may be made of zirconiumphosphate, such as a ZrP of formula Zr(HPO₄)₂ or γZrP of formulaZr(H₂PO₄)₂(HPO₄). It is also possible to treat the particles based onzirconium, titanium, cerium and/or silicon phosphate with an organiccompound before introduction into the thermoplastic matrix, inparticular with an aminosilane compound, such as, for example,3-aminopropyltriethoxysilane, or an alkylamine compound, such as, forexample, pentylamine.

The PA 6 barrier layer composition according to the invention cancomprise from 0.01 to 30% by weight of nanometric lamellar particleswith respect to the total weight of the composition, preferably lessthan 10% by weight, more preferably from 0.1 to 10% by weight, morepreferably still from 0.1 to 5% by weight, particularly from 0.3 to 3%by weight, very particularly from 1 to 3% by weight.

The PA 6 composition can, in addition, optionally include particles ofnanometric lamellar compound having an intercalation agent which isintercalated between the lamellae of the particles and/or an exfoliationagent which is capable of exfoliating the lamellae of the particles, soas to completely separate the lamellae from one another in order toobtain individual lamellae. These particles can be nanometric lamellarcompounds based on zirconium, titanium, cerium and/or silicon phosphateor any other type of compound, such as: natural or synthetic clays ofthe smectite type, such as, for example, montmorillonites, laponites,lucentiles or saponites, lamellar silicas, lamellar hydroxides, acicularphosphates, hydrotalcites, apatites and zeolitic polymers. Theintercalation and/or exfoliation agents can be chosen from the groupconsisting of: NaOH, KOH, LiOH, NH.sub.3, monoamines, such asn-butylamine, diamines, such as hexamethylenediamine or2-methylpentamethylenediamine, amino acids, such as aminocaproic acidand aminoundecanoic acid, and amino alcohols, such as triethanolamine.

In general, tube 12 may comprise one or more layers of one or moreflexible materials such as an elastomer or a plastic. Thus, the innersurface material of the tube may be chosen to withstand the fluids andenvironmental conditions expected within the hose. According to anembodiment of the invention, the inner tube is of a singlenon-fluorinated rubber formulation. The rubber formulation of the innertube may be based on ECO, NBR, NBR-PVC blends, HNBR, TPE, or the likeand may be formulated in accordance with known methods of rubbercompounding. The rubber formulation may include a blend of elastomers,such as a blend of high- and low-acrylonitrile grades of NBR with PVC.The tube rubber composition may advantageously include adhesionpromoter, such as a reactive resin system such as or equivalent toresorcinol, a formaldehyde donor, and silica this is commonly referredto as an “RFS” adhesion system, examples of which are disclosed in Th.Kempermann, et al., “Manual for the Rubber Industry,” 2d Ed., Bayer AG,Leverkusen, Germany, pp 372 & 512-535 (1991) which is herebyincorporated herein by reference. The main purpose of this “RFS” systemis to enhance adhesion between tube 12 and PA 6 barrier layer 14.

In general, tie layer 20 may be used to facilitate bonding between thePA 6 and the cover layer and/or the textile or wire reinforcement. A tielayer may comprise a rubber composition based on ECO, NBR, NBR-PVC,HNBR, TPE, or the like. The main purpose of the tie layer is to provideor promote adhesion, which is especially important when the cover doesnot have an adhesion promoter such as the “RFS” system and/or does notnaturally adhere to well to the PA 6 layer. Both the inner tube and thetie layer may utilize the same rubber composition. The tie layer rubbercomposition may incorporate any suitable adhesion promoter or adhesionsystem, such as the RFS system described above. A tie layer may also becalled a friction layer. A tie layer could be an adhesive coating.

In general, cover 16 may be made of one or more suitable flexibleelastomeric or plastic materials designed to withstand the exteriorenvironment encountered. According to an embodiment of the invention,the outer cover is of a single non-fluorinated rubber formulation. Therubber formulation of the outer cover may be based on HNBR, CSM, CR,ECO, EVM, ACM, EAM, NBR-PVC, or CPE, and the like, which may beformulated with other ingredients in accordance with known methods ofrubber compounding. Tube 12 and cover 16 may be made of the samematerial composition or of different compositions. Preferably the coveris ozone resistant.

A preferred material for the inner tube and the tie layer is a rubbercomposition based on ECO. Suitable ECO includes epichlorohydrinhomopolymer, or a copolymer of ethylene oxide and epichlorohydrin. Apreferable ECO grade is a terpolymer including allyl glycidal ether(“GECO”), which provides sulfur- or peroxide-curable diene cure sites inaddition to the typical de-chlorination cure sites of theepichlorohydrin. The secondary diene cure site may contribute to reducedpermeation and improved sour gas resistance.

It should be understand that while a preferred embodiment includes nofluoropolymer components, that for very severe applications or verystringent permeation or environmental requirements, fluoropolymers mayadvantageously be included in one or more layers of the hoseconstruction or as a tie layer.

As shown in FIG. 1 and mentioned above, reinforcement member 18l may bepresent in the hose. The reinforcement may be applied directly ontointermediate layer 14 and thereby at least a portion of thereinforcement may be in contact with the intermediate layer. Preferably,tie layer 20 is first applied to intermediate layer 14. Then,reinforcement 18 is applied onto tie layer 20. Outer cover 16 maysubstantially surround or penetrate reinforcement member 18 and also bein contact with at least a portion of the intermediate layer or incontact with tie layer 20. The outer cover may advantageously be arubber composition formulated to bond to a textile or wire reinforcementand/or to the PA 6 intermediate layer. For example, the outer cover maybe CSM or CM elastomer with silica filler and resorcinol-formaldehyde orphenol-formaldehyde resin as an RFS adhesion promoting system. Apreferred arrangement is to apply a spiraled, knitted or braided layerof textile or wire onto the PA 6 barrier layer or onto a tie layer. In aspiral construction, for example, the spiraled layer may comprise twolayers, each applied at or near the so-called lock angle or neutralangle of about 54° with respect to the longitudinal axis of the hose butwith opposite spiral directions. However, the hose is not limited tospiral constructions. The textile or wire layer may be knit, braided,wrapped, woven, or non-woven fabric. It has been found that textilefiber or yarn used in combination with an ECO tube, PA 6 barrier, andCSM cover, results in a remarkable increase in burst pressure rating forthe resulting hose. Thereby, the need for reinforcement in embodimentsof the present hose may be reduced. Many useful fibers forreinforcement, such as nylon, polyester (PET) or aramid, may benefitfrom an adhesive treatment or another tie layer in order to achieveadequate bonding among the layers of the hose. Useful reinforcementmaterials include polyester, aramid, polyamide or nylon, rayon, vinylon,polyvinyl alcohol (“PVA”), metallic wire, and the like.

Hose 11 may be formed by methods such as molding, wrapping, and/orextrusion. For example, an inner tube may be extruded, then anintermediate layer of PA 6 may be extruded onto the inner tube. Then atie layer may be extruded or applied to the intermediate layer.Preferably the barrier layer of PA 6 is disposed in the hose byextruding a tubular layer of PA 6 onto the inner tube in a continuousmanner with no overlap or seam. A textile or wire reinforcement may thenbe spiraled, knit, wrapped, or braided onto the intermediate layer or atie layer may be applied before the textile reinforcement. Then a coverstock may be applied. Alternately, the layers may be built up on amandrel. Finally, the assembly may be cured or vulcanized, by heat orradiation, on a mandrel, for example in an oven or a steam vulcanizer,or wrapped, and/or according to other methods available to those skilledin the art. Preferably curing is done at a temperature below the meltingtemperature of the PA 6 layer.

One hose construction has been illustrated in FIG. 1. It should beunderstood that a wide variety of other constructions may be utilized incarrying out the invention. For example, the hose may have additionalinner, outer, or intermediate layers comprising plastic or elastomericcompositions for particular purposes such as fluid resistance,environmental resistance, or physical characteristics and the like. Asanother example, additional textile or metal reinforcements, jackets,covers or the like may be utilized as needed or desired. Helical wiresmay be built into the hose wall or utilized inside the hose for collapseresistance. Textile reinforcements may be treated with adhesives,friction or skim layers, or the like.

Instead of extruding the barrier layer as a tube, films or tapes ofbarrier layers may be wrapped around an inner tube and the laps fused ormelted to create a continuous barrier layer. Curved hose could be madewith PA 6 barrier materials as well. For example, in a two step process,an uncured hose may be placed onto a curved mandrel or placed into amold for vulcanization so that the hose would retain a curved shapedthereafter. Likewise, other known molding techniques may be utilized.

In operation, a fuel hose may be a component of a hose assembly or afuel line assembly or a fluid transfer system. A fluid transfer systemgenerally comprises a hose, and at one or more ends of the hose, one ormore clamps, couplings, connectors, tubing, nozzles, and/or fittings,fluid handling devices, and the like. By way of example, FIG. 2 is aschematic representation of a hose system employing embodiments of theinventive hose. In particular, FIG. 2 represents a typical automotivefuel system. Referring to FIG. 2, fuel tank 31, fuel pump 33, surge tankor reservoir 38 and fuel pump 39 may be connected by one or more fuelhose sections 35 and 36, provided by embodiments of the invention. Fuelreturn line 34 may also include a section of the present inventive hose.Hose sections 35, 36, and 34 may be of a low pressure constructionemploying embodiments of the present invention. Medium or high pressurehose section 37, according to an embodiment of the invention, may beused to connect fuel pump 39 to fuel rail 32 with its injectors and tofuel pressure regulator 40. It should be understood that a fuel systemutilizing the inventive hose is not limited to automotive vehiclesystems, but may include fuel transfer systems throughout the fuelsupply chain, or fuel systems in marine applications, aviation, and thelike, or anywhere else very low permeability flexible hose is desirable.For example, the inventive hose may be also useful for transportingother fluids, including gases, including for example oxygen, hydrogen,or carbon dioxide, liquefied or gaseous propane or natural gas, otherfuels, and refrigerants, and the like, with minimal permeation losses.

Some examples based on film and hose testing follow which serve toillustrate the advantages of the present invention. Film testing wascarried out on two films of impact-modified PA 6 according to theinvention, i.e., Ex. 1 with Technyl® C 548B and Ex. 2 with C 536XT fromRhodia; and for comparison on two other films according to the art:Comp. (i.e., comparative) Ex. 2 with THV (THV 500G from Dyneon, a 3MCompany) and Comp. Ex. 3 with EVOH (EVAL M100B from Kururay Co. Ltd. andEVAL Company of America.). The test used 0.13-mm (5-mil) films of eachmaterial in Thwing-Albert permeation cups, under conditions including60° C. with CE10 (a mixture of ASTM Fuel C with 10% ethanol).

The same film materials, at the same thickness as the film tests, wereincorporated into hose for Hose Permeation tests run at 60° C. and witha variety of test fuels, including ASTM Fuel C, CE10, and CM15 (amixture of Fuel C with 15% methanol). Permeability of a hose wasmeasured with a number of fuel-type fluids using the reservoir method inSAE J30 Section 9 but at an elevated temperature of 60° C. The methoduses stationary fuel from a closed reservoir with a metallic plug toseal the end of the hose. Every week, the fuel was drained from the hoseinto the reservoir so fresher fuel would then be returned into the hose.The test duration was for 1000 hours of conditioning plus 10 days ofpermeation measurement. This method was used as a convenient way toscreen constructions and to approximate the permeation measurementconditions of SAE J1737, a preferred standard in fuel permeationmeasurements. It may be noted that the method of SAE J1737 involvescirculating hot fuel or vapor under controlled pressure. The hoseexamples were also tested with the procedure of SAE J1737 at 40° C.using indolene fuel.

As mentioned above, and illustrated in Table 2, the melt flow rate ofthe preferred PA 6 is relatively low, i.e., the viscosity is relativelyhigh. The processing of the hose, in particular the extrusion of thebarrier layer, was carried out with a rather large die (both gap anddiameter), no breaker plate, at the highest recommended barreltemperatures 280-315° C. (550-600° F.), with a high shear screw, andusing the drawn down approach to reduce the barrier layer thickness.These conditions permitted extrusion of the high-viscosity materialwithout problems. In particular, the extrusion gap was about 1.5 mm (1/16 inch), and the draw down ratio was 19 to 64% depending on hosesize.

TABLE 2 Barrier Material Test conditions Standard Melt Flow Index Ex. 1C 548B (PA 6) 275° C./5-kg load ISO 1133  3-8 [g/10 min] Ex. 2 C 536XT(PA 6) — — — Comp. Ex. 3 THV 500G (THV) 265° C./5-kg load ASTM D12388-12 [g/10 min] Comp. Ex. 4 Eval M100B (EVOH) 275° C./2.16-kg load ISO1133 1-3.5 [g/10 min] 

The permeation results for both film and hose are shown in Table 3. Foreach of the tests reported, the PA 6 material had much betterperformance (lower permeation rate) than THV or EVOH. In addition, the C548B PA 6 material exhibited no problems with kinking during processingfor all sizes of hose built thus far ( 3/16″, ¼″, 5/16″, ⅜″, and ½″ ID).The fuel hose utilizing C 548B PA 6 material as a barrier does pass thekink resistance test in SAE J30R7 and R14 while the EVOH barrier hosefailed those tests. The C 548B PA 6 material exceeds the permeationresistance of competitive materials as well as the requirements of manyof the current governmental standards.

TABLE 3 Comp. Comp. Properties Method Units Ex. 1 Ex. 2 Ex. 3 Ex. 4Barrier Material Technyl ® Technyl THV EVAL C 548B C536XT 500G M100B PA6 PA 6 EVOH Film Permeation Thwing-Albert g/m²/d 50 35 180 65, 40 60°C./CE10 Hose Permeation SAE J30 g/m²/d 2 — 36 21 60° C./Fuel C HosePermeation SAE J30 g/m²/d 4 — 70 40 60° C./CE10 Hose Permeation SAE J30g/m²/d 18 — 49 58 60° C./CM15 Hose Permeation SAE J1737, g/m²/d 0.9 — 8  1.9 40° C./Indolene

It should also be noted that the example hoses were constructed with6-mm (¼-inch) inside diameter and in accordance with an embodiment ofthe present invention with an ECO (GECO) rubber inner tube including anRFS adhesion promoting system 1.0-mm (40-mil) thick; a 0.13-mm (5-mil)thick intermediate barrier layer; a tie layer of the same ECO rubber asthe tube but 0.5-mm (20-mil) thick; a PET spiral-wrapped double-layeryarn reinforcement; and a CSM rubber outer cover layer 1.0-mm (40-mil)thick. Comp. Ex. 3 represents a commercial fuel hose having an NBR tube1-mm thick, a 0.13-mm thick THV barrier, an NBR tie layer 0.5-mm thick,a nylon reinforcement, and a CSM cover 1.25-mm thick. Comp. Ex. 3 wasdesigned to meet the permeation requirements of SAE J30R11 or R12 forfuel hose. Comp. Ex. 4 is based on co-pending U.S. patent applicationSer. No. 11/938,139 with EVOH (EVAL M100B) as the barrier layer butotherwise similar construction to Ex. 1 except the reinforcement wasnylon and the cover was 1.25-mm thick.

The results of the permeability testing, presented in Table 3, show thedramatic improvement in impermeability of the inventive Example hoseover the comparative hoses. As a general observation, it appears thatthe inventive hose is about 2 to 10 times lower in permeability tovarious fuels than the best comparative hoses.

The permeation rate for the inventive example may also be compared tosome of the patents mentioned in the above background section, as wellas to various fuel hose standards such as SAE J30 or SAE J1527 formarine applications. For example, SAE J30 R6, R7,-R8 and R9 applies toconventional rubber hoses without barrier layers which are tested atroom temperature, with closed reservoir and no circulation. R9 requiresa permeability to Fuel C of <15 g/m²/day. R6, R7, and R8 requirepermeability to Fuel C of <600, <550, and <200 g/m²/day, respectively.SAE J1527 Class 1-15 requires <15 g/m²/day for Fuel CE10. SAE J30 R11and R12 apply to low-permeation hoses which are tested according to SAEJ1737 at 40° C. and 60° C. respectively, under pressures of 14.5 kPa(2.1 psi) and 0.2 MPa (29 psi) respectively, and with circulation, andrequire a permeability for CM15 (a much more aggressive test fuel thanFuel C) of <25 g/m²/day for category A (the most stringent rating). Thetemperature increase alone from room temperature to 40° C. is expectedto increase the permeability by a factor of about 10 times, partly dueto increased diffusion rate and partly due to increased vapor pressureof fuel in the closed reservoir. The present stationary fuel test hasbeen carried out at 60° C. which is expected to increase thepermeability by an additional factor of about 20 times over a 40° C.test, all other factors constant. The pressure of the R11 test conditionis probably not much different from the vapor pressure in a closedreservoir at elevated temperature. However, the effects of circulationand pressure in the R12 test may be estimated to increase thepermeability by a factor of up to about 20 times over a stationary testat 40° C. Thus, the inventive hose, having permeability to stationaryCM15 fuel of about 0.5 g/m²/day at 60° C., is estimated to be about 1000times better (25×20/0.5) than required by the R11 standard and tocomfortably meet the R12 standard. Thus, the inventive hose is wellsuited for handling the increased impermeability demands associated withalcohol-containing fuels.

Actual testing according to SAE J1737 at 40° C. with indolene at 0.2 MPa(29 psi) pressure was carried out on the Example inventive hose and on acomparative fluoropolymer barrier hose. The inventive hose exhibited apermeation rate of 0.9 g/m²/day. The comparative fluoropolymer barrierhose exhibited a permeation rate of 8 g/m²/day. Thus, the inventive hosemay provide a permeability to CM15 or CE10 Fuel of less than 2 g/m²/dayat 40° C. or less than 40 g/m²/day at 60° C. when tested according toSAE J1737, or less than 20 g/m²/day at 60° C. when tested according to aSAE J30 Section 9.

For a comparison to other barriers, the laminate barrier of U.S. Pat.Publication No. 2003/87053 exhibited permeability to CE10 fuel of 1.6g/m²/day at room temperature. As mentioned above, increasing thetemperature from room temperature to 60° C. is expected to increase thepermeation by a factor of 200 times. Thus, the example inventive hose isabout 100 times better than the laminate of U.S. Pat. Publication No.2003/87053.

Comparison with the hose disclosed in U.S. Pat. No. 6,941,975, whichexhibited permeability of 3.94×10⁻⁵ g/cm/day for refrigerant 134A at 90°C., is difficult without information on the hose diameter or area per cmlength. Nevertheless, it is believed that the inventive hose would be atleast comparable to that hose in permeability, while the inventive hoseadvantageously accomplishes low permeation without use of amulti-layered barrier. Thus, an embodiment of the inventive hose mayalso be useful for refrigerant applications.

The example hoses were also tested for bursting pressure. The typicalfuel hose application generally requires a working pressure of less than0.7 MPa (100 psi). With typical spiraled nylon reinforcement, rubberhose generally exhibits a burst pressure of about 1.7 to 2.4 MPa (250 to350 psi). With the addition of the 0.13-mm (5-mil) layer of PA 6, theinventive Example 1 hose with PET reinforcement exhibited a burstpressure of about 4.1 MPa (600 psi), somewhat higher than expected.Thus, the need for reinforcement may be reduced in the inventive hose,or the working pressure significantly increased.

Flexibility testing at low temperatures was carried out on the inventiveexample hose. The inventive fuel hose of Example 1 met the SAE J30R14cold flexibility standard, kink resistance, and permeation requirements.

In the course of investigating embodiments of the invention, it wasdiscovered that bio-diesel fuels were unexpectedly more aggressivepermeants than petroleum-based or conventional diesel, particularly inconventional NBR or HNBR or ECO type fuel hoses, resulting failures ofthe outer cover, particularly CSM, CR, or EPDM covers. Inventive hosessuch as Ex. 1 and Ex. 2 above have been found to solve this problem. Italso believed that the barriers in the comparative examples would alsosolve this problem with bio-diesel. Thus, another invention orembodiment is the use of a barrier layer as described herein in amulti-layer bio-diesel fuel hose to solve the problem of bio-dieselpermeation.

It should be understood that the inventive concept could also beadvantageously utilized in a hose having a fluoropolymer inner tubeand/or outer cover by incorporating an intermediate PA 6 barrier layer.The permeation rate should be excellent, although the cost would besignificantly higher than for a non-fluoroelastomer hose at currentelastomer prices.

The PA 6 may preferably be of sufficient thickness, or an effectivethickness, to provide reduced permeation of a specified or predeterminedfuel or fuel component of less than or equal to 15 grams per squaremeter per day tested for example according to SAE J1737 at a temperaturesuch as at 25° C., 40° C. or 60° C. Preferably the PA 6 is one of thespecific grades mentioned herein, or with a set of characteristics asdescribed herein, or most preferably Technyl® C 548B, which is soldunder that trademark by Rhodia Engineering Plastics.

In another embodiment, the inventive hose may comprise two or morelayers, or preferably two to five layers, including a thin layer of PA 6as described herein. The PA 6 layer may preferably have a thickness ofup to 0.010 inches (0.25 mm). The PA 6 may preferably be of sufficientthickness, or an effective thickness, to provide reduced permeation of aspecified or predetermined fuel or fuel component of less than or equalto 15 grams per square meter per day. The predetermined fuel componentmay be methanol or ethanol or fatty acid derivatives, such as used infuels such as bio-fuels or flex-fuels. The predetermined fuel may beselected from fuels such as indolene, gasoline, biodiesel, diesel,alcohols, and alcohol-containing fuels without limitation. The otherlayers may be or include, without limit, a reinforcement such as atextile or wire, a different thermoplastic material including forexample a TPE, a thermoset material such as a rubber or a crosslinkedthermoplastic. Thus, embodiments of the invention include, withoutlimitation, non-reinforced hose, for example, having two, three, or morelayers; or reinforced hose having four, five, or more layers. FIG. 3illustrates such a two-layer embodiment in the form of hose or tubing140 comprising thin layer 142 of PA 6 and second layer 144 of othermaterial such as rubber or plastic. FIG. 1 illustrates a five-layerembodiment as discussed earlier.

The resulting inventive hose according to one or more embodiments of theinvention may advantageously be used, without limitation, for fueltubing, fuel hose, fuel vapor hose, vent hose for fuel or oil, airconditioning hose, propane or LP hose, curb pump hose, large insidediameter filler neck hose or tubing, marine fuel hose, fuel injectionhose, or the like, including diesel, bio-diesel, and other oil-likefuels or blends of any of the foregoing.

Hose embodiment for aggressive fuels at extreme conditions.

Surprisingly, it was discovered that the above presented embodimentswere not sufficient for certain biofuels, in particular for the mostaggressive biofuels, such as that designated B20. “B20” means a mixtureof 20% bio-diesel and 80% petroleum-based diesel fuel. “B100” likewisemeans 100% bio-diesel, and so forth. It has been found that B20 is muchmore aggressive to fuel hose than B100, so that the targeted hotperformance, such as target permeation rate, was not achieved by fuelhoses with ECO or NBR rubber formulations for the tube and/or covermaterials. Such hoses had to be limited to use at temperatures of 100°C. or below. In particular, this applies to fuel injection hoses withhigh pressure and high temperature requirements.

Thus, there is a need for fuel line hoses which can handle highertemperatures, lower gasoline permeation, bio-fuel capability, and highpressure capability as compared to traditional fuel lines or even lowpermeation fuel lines. Traditional fuel lines (SAE J30R7) are lowtemperature, high gasoline permeation, low pressure, and have limitedresistance to bio-fuels (particularly B20 at elevated temperatures).They are however, very cost competitive. Low permeation fuel lines (SAEJ30R14—barrier type) address the gasoline permeation issue, but are lowtemperature, low pressure, with limited bio-fuel capability (typicallyNBR tube). They are moderately priced. Fuel Injection hoses (meeting SAEJ30R9, SAE J30R12) are high temperature, low permeation, high pressureconstructions that have full bio-fuel capability, but are very expensivebecause of the use of FKM materials.

Typical hose constructions use NBR (nitrile) tube materials, which areinsufficient in several ways for this type of application. (1)Permeation resistance -Permeation rates are much higher than EPA/CARBallow (15 grams/square meter/day). In addition, bio-fuel will permeatethrough the tube layer to the hose surface. (2) Temperatureresistance—NBR is sufficient only up to ˜125° C. (257° F.)

Bio-Fuel Resistance—Bio-fuels can be very aggressive at B20 blends,particularly at elevated temperatures. NBR is degraded in these fluidsat elevated temperatures.

Fuel Injection hoses typically utilize FKM tube materials, but FKM isextremely expensive. It has very good permeation resistance to bothgasoline and bio-fuels. It is very resistant to gasoline and dieselfuel, including bio-fuel blends. It is not significantly degraded by B20blends at elevated temperatures. It has temperature resistance up to135° C. continuous, and 150° C. intermittent.

According to an embodiment of the invention, a five-layer hoseconstruction was found to provide excellent performance as a fuelinjection hose for biofuels such as B20 and other aggressive fuels attemperatures up to about 135° C. According to this embodiment, thelayers of the hose from the inside out are: (1) a tube made of an HNBRrubber composition, (2) a barrier layer of the special nylon asdescribed herein (as a preferred barrier, Technyl C548B), (3) a frictionlayer (i.e. elastomeric tie layer) also of HNBR rubber formulation(which may be the same as the tube), (4) a reinforcing layer (which maypreferably comprise aramid fibers or yarns), and (5) a cover made of arubber composition based on an elastomer blend of EVM and CPE (which mayalso be used as the friction layer instead of HNBR). The basicconstruction may thus be a five layer hose construction, consisting ofan HNBR tube layer, a C548B plastic barrier layer, an HNBR frictionlayer, an aramid reinforcement layer, and an EVM/CPE blend cover layer.This combination gives excellent fuel resistance with the temperatureand pressure resistance needed for these applications.

This hose construction largely meets the SAEJ30 specification, howeverit does not neatly fit into any of the current 14 classificationscurrently in that specification. As a result this hose is considered tobe in the same spirit as low permeation specifications R9, R11, R12, andR14, however it will also encompass aspects of the currently proposedR13 biodiesel section.

This hose embodiment is intended to meet the demands of fuel injectionsystems and is useful in the transportation of gasoline, ethanol,methanol, ethanol extended gasoline, diesel fuel, Biodiesel includingSoybean methyl ester (SME), Rapeseed methyl ester (RME), and Palm methylester (PME) that meets ASTM D6751, highly aromatic oils or paraffinicoils, as well as the fuel/oil vapor present in either the fuel systemsor the crankcase of internal combustion engines. This hose is preferredfor liquid fuels only, and is not intended for gaseous fuels such aspropane, methane, or natural gas.

The HNBR tube is preferably a zinc-free elastomeric composition. TheHNBR tube layer and the thermoplastic barrier layer are resistant tochemical attack, swelling, and permeation. This construction alsoincludes an oil, semi-fuel, and ozone resistant outer cover based on ablend of EVM and CPE. Table 4 shows some typical useful dimensions forthis hose embodiment.

HNBR (Hydrogenated nitrile) has a saturated polymer backbone, whichgives excellent chemical resistance, and high temperature stability.HNBR is highly resistant to fuels (gasoline, diesel fuel and bio-dieselblends). Bio-fuels can be aggressive at certain blends (B20particularly), especially at elevated temperatures. HNBR hasdemonstrated stability when aged in B20 blends at elevated temperatures(135° C.). When combined with the C548B barrier layer, the hoseconstruction, the gasoline permeation rate is extremely low (˜1gram/square meter/day per SAE J1737 at 40° C.), and permeation ofbio-diesel on a 6-month equivalent test is not detectable. The entirehose construction is intended for use at elevated temperatures (135° C.continuous, 150° C. intermittent).

Material and performance testing was carried out on this fuel hoseembodiment and its various components. All tests are to be conducted inaccordance with ASTM D380, standard test methods for rubber hose unlessotherwise specified. Table 5 shows a specification for material andperformance testing of an HNBR tube compound useful in this embodiment.Table 6 shows a specification for material and performance testing of anEVM/CPE cover compound useful in this embodiment.

Additional specifications may be met by this hose embodiment, asfollows. The minimum burst pressure for all sizes through 12.7mm (½″ ID)may be 8.0 MPa (1160 psi). The maximum working pressure for all sizesthrough 12.7mm (½″ ID) may be 1.55 MPa (225 psi). This hose may besuitable for use in normal continuous operating temperatures of −40 to135° C. (−40 to 275° F.) with intermittent use up to 150° C. (302° F.).However, extended periods at 150° C. (302° F.) may significantly reducehose life.

TABLE 4 Dimensions & Minimum Bend Radius: Hose Minimum Size InsideDiameter Outside Diameter Bend Radius 3/16″ 4.36 mm-5.16 mm  9.74mm-10.90 mm 55 mm (2.16″) (0.172″-0.203″) (0.384″-0.429″) 5 mm 4.60mm-5.40 mm  9.98 mm-11.14 mm 57 mm (2.24″) (0.181″-0.213″)(0.393″-0.439″) ¼″ 5.95 mm-6.75 mm 12.11 mm-13.27 mm 65 mm (2.56″)(0.234″-0.266″) (0.477″-0.525″) 5/16″ 7.54 mm-8.34 mm 13.70 mm-14.86 mm75 mm (2.95″) (0.297″-0.328″) (0.539″-0.585″) ⅜″ 9.13 mm-9.93 mm 15.29mm-16.45 mm 85 mm (3.35″) (0.359″-0.391″) (0.602″-0.647″) ½″ 12.30mm-13.10 mm 19.05 mm-20.63 mm 120 mm (4.72″) (0.484″-0.516″)(0.750″-0.812″)

TABLE 5 After Aging After aging After aging After 168 hr After aging 70hr at 150° 168 hr at 168 hr at at 150° C. in After 168 hr 168 hr at TubeC. in ASTM 23° C. in 23° C. in Bio-diesel³ at 135° C. 135° C. OxidizedCharacteristics Original IRM 903 Oil Fuel C¹ Fuel G² (SME) in B20/D80⁴Dry Heat Fuel⁵ Ultimate 10.34 MPa +/−50% −45% 5.5 MPa 6.90 MPa 6.90 MPa6.90 MPa −35% Tensile (1500 psi) Change change (798 psi) (1000 psi)(1000 psi) (1000 psi) change min min Actual min Actual min Actual minActual Elongation 200% min +/−50% −45% 150% min 150% min 150% min 150%min −40% at break Change change Actual Actual Actual Actual change ShoreA 70 ± 15 +/−20 — — — — — — Hardness Points Change Volume Swell — +20%Max +50% max +55% max +30% max +25% max — — (% change) ¹Reference Fuel Cis comprised of 50% Iso-octane + 50% toluene - per SAEJ30 December 2008Appendix A ²Reference Fuel G is comprised of 85% Fuel D (60%Iso-octane + 40% Toluene) + 15% anhydrous denatured ethanol - per SAEJ30December 2008 Appendix A. ³Biodiesel: Soybean Methyl Ester that meetsASTM6751 ⁴B20/D80 test fuel: 80% ASTM D975 Grade 2-D S15 Diesel with 20%ASTM 6751 Soybean methyl ester ⁵Oxidized fuel testing per SAEJ30R7December 2008 section 6.18.

TABLE 6 After Aging After aging 70 hr at 150° 168 hr at After agingCover C. in ASTM 150° C. 24 hr at 23° Characteristics Original IRM 903Oil Dry Heat C. in Fuel B⁶ Ultimate Tensile 8.28 MPa 6.90 MPa 6.90 MPa —(1200 psi) (1000 psi) (1000 psi) min min Actual min Actual Elongation175% min 150% min 100% min — at break actual Actual Shore A Hardness 80+/− 5 — — — Volume Swell — +75 max — +75 max (% change) ⁶Reference FuelB is comprised of 70% Iso-octane + 30% Toluene - per SAEJ30 December2008 Appendix A.

The inventive hose may be subjected to an aging period of 1000 hours at135° C. in dry air while bent to the minimum bend radius. After agingand within 6+/−2 seconds the hose may be brought to a straight position.The hose cover should show no cracking, charring, or disintegration. Thehose may then be subjected to an air-under-water proof test at themaximum continuous working pressure specified for a period of 3 minutesand show no signs of leakage.

Fuel-aged cold flexibility may be tested as follows. Hose shall befilled with ASTM D471 Fuel C and conditioned for 70 hours at 23+/−1° C.hose shall then be drained and conditioned in a straight position for 5hours at −40° C. after conditioning and within 10+/−2 seconds the hoseshall be bent around a mandrel whose radius is equal to the minimum bendradius specified for the respective hose size and as a result may notbreak or crack. The hose may then be subjected to an air-under-waterproof test at the maximum continuous working pressure specified for therespective hose size for a period of 3 minutes and may show no signs ofleakage.

Rate of fuel permeation may be tested as follows. The fuel permeationusing CE10 fuel should not exceed a maximum rate of 15 g/m² day whenperformed using the reservoir method discussed in SAE J30 (8 days @23°C.). Also, this hose typically meets and exceeds CARB requirements forsmall off-road engines and as such may display a certification number onthe hose lay line. Reference Fuel CE10 is comprised of 80% Fuel C (50%Iso-octane+50% Toluene)+10% anhydrous denatured ethanol.

Vacuum resistance may be tested as follows. Hose may be subjected to atest vacuum for 15 to 30 seconds while in a straight position. The testvacuum may be 81 kPa for hose sizes 9.52 mm and smaller and 34 kPa forhoses size larger than 9.52 mm. The outside diameter of the hose may notbe reduced by more than 20% at any time during the test.

Adhesion may be tested as follows. The load required to separate a 25.4mm (1.0 in) width of any adjacent layers of the multi-layer constructionshould be greater than 35.6 N (8 lb).

Ozone Resistance may be tested as follows. Hose may be conditioned in anatmosphere with an ozone partial pressure of 100 mPA (100 parts of ozoneper 100 million parts of air) at standard atmospheric conditions for 336hours at 40° C. while bent to the minimum bend radius. At the conclusionof the test the hose cover should show no evidence of cracking ordeterioration when viewed under 7× magnification while still in thestressed condition.

Extractables may be tested as follows. Using the method to determineextractable as outlined in SAE J30 the maximum total value should be7.75 g/m².

Hoses constructed according to this embodiment passed theabove-described tests and met the specifications described.

Although the present invention and its advantages have been described indetail, it should be understood that various changes, substitutions, andalterations can be made herein without departing from the spirit andscope of the invention as defined by the appended claims. Moreover, thescope of the present application is not intended to be limited to theparticular embodiments of the process, machine, manufacture, compositionof matter, means, methods, and steps described in the specification. Asone of ordinary skill in the art will readily appreciate from thedisclosure of the present invention, processes, machines, manufacture,compositions of matter, means, methods, or steps, presently existing orlater to be developed that perform substantially the same function orachieve substantially the same result as the corresponding embodimentsdescribed herein may be utilized according to the present invention.Accordingly, the appended claims are intended to include within theirscope such processes, machines, manufacture, compositions of matter,means, methods, or steps. The invention disclosed herein may suitably bepracticed in the absence of any element that is not specificallydisclosed herein.

What is claimed is:
 1. A fuel hose suitable for biofuel oralcohol-containing fuel comprising: an HNBR rubber inner tube; a rubberouter cover based on an elastomer blend consisting of EVM and CPE; anintermediate barrier layer consisting essentially of an impact-modifiedpolyamide 6; and a textile reinforcement disposed between said barrierlayer and said outer cover, wherein the radial thickness of the barrierlayer is in the range of from 0.025 mm to 0.76 mm, wherein saidpolyamide 6 has a branched molecular structure, a flexural modulus offrom 1 to 2 GPa, a tensile elongation at break of about 100% or more;wherein the hose has at least one of a permeability to gasoline of about1 g/m²/day or less at 40° C. and a permeability to B20 biofuel of lessthan 1 g/m²/day at 40° when tested according to SAE J1737.
 2. The fuelhose of claim 1 comprising only non-fluoropolymer-based layers.
 3. Thefuel hose of claim 1 wherein said barrier layer is a seamless, tubularlayer.
 4. The fuel hose of claim 1 further comprising an elastomeric tielayer between said barrier layer and at least one of said rubber tubeand rubber cover layers.
 5. The fuel hose of claim 1 wherein saidpolyamide 6 exhibits the following physical properties: Tensile modulusaccording to ISO 527 type 1A of about 1850/1000 MPa; Tensile strength atyield according to ISO 527 type 1A of about 55/45 MPa; Tensile strain atbreak according to ISO 527 type 1A of about 150/220%; Flexural modulusaccording to ISO 178 of about 1750/850 MPa; Flexural maximum stressaccording to ISO 178 of about 70/45 MPa; and Either Charpy notchedimpact strength according to ISO 179/1eA of about 92/NB kJ/m2, whereinNB signifies No Break, or Izod notched impact strength according to ISO180/1A of about 90/NB kJ/m2, wherein NB signifies No Break; wherein iftwo values are listed, the first is for Dry As Molded material, and thesecond value is for material conditioned according ISO
 1110. 6. A hosecomprising: an HNBR rubber inner tube; a rubber outer cover based on anelastomer blend consisting of EVM and CPE; an intermediate barrier layerconsisting essentially of an impact-modified polyamide 6; and a textilereinforcement disposed between said barrier layer and said outer cover,wherein the radial thickness of the barrier layer is in the range offrom 0.025 mm to 0.76 mm, wherein said polyamide 6 has a branchedmolecular structure, a flexural modulus of from 1 to 2 GPa, a tensileelongation at break of about 100% or more; wherein the hose has at leastone of a permeability to gasoline of about 1 g/m²/day or less at 40° C.and a permeability to B20 biofuel of less than 1 g/m²/day at 40° whentested according to SAE J1737.
 7. The hose of claim 6 further comprisingan HNBR rubber tie layer disposed between said barrier layer and saidreinforcement.
 8. The hose of claim 6 further comprising an EVM/CPEblend rubber tie layer between said barrier layer and saidreinforcement.
 9. A hose system comprising: at least one length of hoseaccording to claim 6 and at least one fitting, clamp, or fluid-handlingdevice.
 10. The hose system of claim 9 wherein said polyamide 6 exhibitsthe physical properties, mechanical properties, and thermal properties:Water absorption according to ISO 62 tested 24 h at 23° C. of about1.20%; Density according to ISO 1183-A of about 1.05 g/cc; Tensilemodulus according to ISO 527 type 1A of about 1850/1000 MPa; Tensilestrength at yield according to ISO 527 type 1A of about 55/45 MPa;Tensile strain at break according to ISO 527 type 1A of about 150/220%;Flexural modulus according to ISO 178 of about 1750/850 MPa; Flexuralmaximum stress according to ISO 178 of about 70/45 MPa; At least oneimpact property selected from: Charpy notched impact strength accordingto ISO 179/1eA of about 92/NB kJ/m2, wherein NB signifies No Break;Charpy unnotched impact strength according to ISO 179/1eU NB/NB kJ/m2;and Izod notched impact strength according to ISO 180/1A of about 90/NBkJ/m2; Melting Temperature according to ISO 11357 of about 222° C.; andHeat deflection temperature at 1.8 MPa according to ISO 75/Af of about55° C.; wherein if two values are listed, the first is for Dry As Moldedmaterial, and the second value is for material conditioned according ISO1110.